Power generation with CO2 capture: Technology for CO2 purification

The goal of this paper is to find methodologies for removing a selection of impurities (H₂O, O₂, Ar, N₂, SO_x and NO_x) from CO₂ present in the flue gas of two oxy-combustion power plants fired with either natural gas (467 MW) or pulverized fuel (596 MW). The resulting purified stream, containing mainly CO₂, is assumed to be stored in an aquifer or utilized for enhanced oil recovery (EOR) purposes. Focus has been given to power cycle efficiency i.e.: work and heat requirements for the purification process, CO₂ purity and recovery factor (kg of CO₂ that is sent to storage per kg of CO₂ in the flue gas). Two different methodologies (here called Case I and Case II) for flue gas purification have been developed, both based on phase separation using simple flash units (Case I) or a distillation column (Case II). In both cases purified flue gas is liquefied and its pressure brought to 110 atm prior to storage.Case I: A simple flue gas separation takes place by means of two flash units integrated in the CO₂ compression process. Heat in the process is removed by evaporating the purified liquid CO₂ streams coming out from both flashes. Case I shows a good performance when dealing with flue gases with low concentration of impurities. CO₂ fraction after purification is over 96% with a CO₂ recovery factor of 96.2% for the NG-fired flue gas and 88.1% for the PF-fired flue gas. Impurities removal together with flue gas compression and liquefaction reduces power plant output of 4.8% for the NG-fired flue gas and 11.6% for the PF-fired flue gas. The total amount of work requirement per kg stored CO₂ is 453 kJ for the NG-fired flue gas and 586 kJ for the PF-fired flue gas.Case II: Impurities are removed from the flue gas in a distillation column. Two refrigeration loops (ethane and propane) have been used in order to partially liquefy the flue gas and for heat removal from a partial condenser. Case II can remove higher amounts of impurities than Case I. CO₂ purity prior to storage is over 99%; CO₂ recovery factor is somewhat lower than in Case I: 95.4% for the NG-fired flue gas and 86.9% for the PF-fired flue gas, reduction in the power plant output is similar to Case I.Due to the lower CO₂ recovery factor the total amount of work per kg stored CO₂ is somewhat higher for Case II: 457 kJ for the NG-fired flue gas and 603 kJ for the PF-fired flue gas.     

Characteristics of azaarenes and dioxins in gases emitted from waste incinerators

In this study, we propose an analytical method to determine the fourteen of azaarenes present in flue gas samples collected according to Japanese Industrial Standard K 0311, which designates the method for the determination of dioxins in flue gas. Azaarenes can be analyzed using the acidic water phase after shaking extraction with dichloromethane, which is unnecessary for dioxin analysis. Flue gas samples were obtained from 24 waste incinerators in Japan, and azaarenes were detected in all the flue gas samples (0.21–3800 μg/m³ _N). The most abundant of the detected compounds were quinoline and isoquinoline. The concentration of azaarenes had a tendency to increase with that of polychlorinated dibenzo-p-dioxins and dibenzofurans. The isomer distribution of heptachloro-dibenzofurans (HpCDFs) was calculated using the computed Gibbs energy of formation (ΔG _f ) obtained by the semiempirical molecular orbital method at various temperatures. The calculated isomer distribution was fitted to the measured value of HpCDFs. It seems that the temperature obtained from the fitting calculations is an indicator of the cooling capacity of the combustion gas in an incinerator. The computed ΔG _f also explained the measured isomer distributions of azaarenes. It is suggested that the isomer distribution of azaarenes in the combustion process is thermodynamically controlled. This work was presented in part at the International Conference on Combustion, Incineration/Pyrolysis, and Emission Control, 2006, Kyoto     

Nanofiltration of concentrated and salted tuna cooking juices

Tuna cooking juice from a Tunisian tuna-processing unit has a high level of polluting load: chemical oxygen demand (COD) is comprised between 4 and 20 g L⁻¹, nitrogen kjedahl (NK) between 0.6 and 3 g L⁻¹ and dry matter between 120 and 160 g L⁻¹. The juice has thus to be treated before being rejected into the environment. This paper considers the nanofiltration (NF) of these concentrated organic/inorganic mixtures using an AFC 30 (NF) membrane. The work focusses on the effect of organic and inorganic matters on the permeate flux and rejections of these matters. For this purpose, mixtures of salt and organic pollution (COD), used as model solutions, were prepared by the dilution of a typical industrial tuna cooking juice. The permeate flux was found to decrease when salt and organic matter concentrations increase. The recovery rate in organic matter decreases with increasing salt or organic matter content and the recovery rate of salt decreases when the COD concentration increases.     

垃圾焚烧飞灰处理处置研究进展

针对作为危险废物的垃圾焚烧飞灰,介绍了近年来国内外对其进行处理处置的研究情况.飞灰的固化/稳定化处理主要从水泥(沥青)固化、熔融固化及化学药剂固化几方面进行论述,飞灰中重金属的提取主要从酸碱浸提、生物浸提、螯合剂浸提及电渗析法提取几方面进行论述.     

铁路运输含硫原油过程中H_2S挥发规律模拟试验研究

以塔河12区含硫原油为研究对象,通过模拟铁路运输原油工况,研究罐内原油中H_2S挥发规律.结果表明,铁路运输过程中原油里H_2S析出浓度与时间的关系近似为6次多项式,并建证了H_2S浓度随时间变化的曲线方程;对影响罐内原油中H_2S挥发的2个主要因素罐内原油温度和罐车振动强度进行了分析.结果表明,罐内原油温度是原油中H_2S挥发的主要影响因素,升高罐内原油温度可以明显增加H_2S的挥发浓度.加大罐车振动强度对原油中H_2S挥发有促进作用,但不明显.     

基于B/S+C/S的矿山安全标准化管理信息系统研究

首先介绍了安全标准化实施的关键步骤、技术特点及其在矿山的应用,通过现场调研、安全培训,危害辨识与风险评价、文件汇编等环节在山西某矿山建立了安全标准化管理信息系统,在此基础上开发了与之相配套的、基于B/S和C/S混合模式的、在局域网上运行的应用软件--矿山安全标准化管理信息系统.系统由统一信息发布平台、即时报警系统、安全记录管理系统、统计分析系统等14个子系统组成.系统的应用提升了矿山安全生产整体水平,实现了矿山安全标准化和信息化.     

基于GSM的远程家庭智能监控系统设计

针对现有的GSM无线网络,介绍了基于GSM的远程家庭智能报警系统的设计及实现方法.利用各种传感器对家中可能出现的各种意外情况进行采集,并通过PT2262/PT2272组建的家中内部无线网络及时向单片机进行中断报警.GSM模块在单片机控制下,利用GSM网络,将各种报警信息通过短信的方式发送到预先设定的手机中,达到了远程无线智能报警的功能.经过测试,该系统经济、可靠、稳定性高.家庭无需为传感器布线,具有广泛的市场推广价值.     

基于网络的智能视频监控系统的设计与实现

基于网络的智能视频监控就是将自动视频分析技术应用到网络视频监控系统中.提出了一种由分析单元、中心服务器和客户端3个部分组成的智能视频监控系统架构方案.通过对定标、DirectShow、TCP/RTP以及Xvid等关键技术在智能视频监控系统的3个组成部分中的作用来说明系统的设计方案,同时指出了实现自动视频分析的各种关键技术和方法.实验结果表明,该解决方案具有良好的可重用性和扩展性.     

辽河稠油热采现场硫化氢的防范与治理建议

硫化氢是一种剧毒和较强腐蚀性的气体,近年来在辽河油田一些地区相继出现,特别是稠油热采区块出现了较高浓度的硫化氢。硫化氢的存在已经威胁到油田的安全生产,并成为油气勘探开发过程中必须解决的问题。本文对辽河油气稠油热现场硫化氢的预防与治理提出了一些建议。     

WTO“稀土案”与中国自然资源出口管制的完善

举世瞩目的 WTO"稀土案"于2014年8月7日终落帷幕。同先前的"原料案"一样,中国还是难逃败诉的命运。上诉机构支持申诉方的大部分指控,再次否决了《1994年关税与贸易总协定》(General Agreement on Tariffs and Trade of 1994,以下简称GATT)第20条对中国《入世议定书》的可适用性,从而确认中国对稀土、钨、钼三种原材料采取的出口税及配额等管制措施违背了WTO相关规则和入世所作的特殊承诺。作为自然资源的进出口大国,在自然资源贸易纠纷(特别是出口管制问题)不断"升温"和WTO争端解决机制运用愈来愈频繁的今天,中国应认真总结和反思这场"稀土保卫战"失利带来的经验教训,以从源头上破解中国出口管制措施在WTO体制下遭遇的法律困境,避免今后类似案件败诉的重现。基于此,本文综合应用案例分析、文本分析、历史分析和比较分析等方法对"稀土案"争讼的焦点和争端解决机构(DSB)的裁决意见做了详尽的透析,结果发现此案中DSB的审理不同程度存在着解释僵化、无视中国缔约真意及主观随意、前后矛盾等失范之处,对中国颇为不公。不过,该案也从另外一方面暴露出中国出口管制立法的疏漏与实施缺陷。是故,本文建议中国:1请求部长级会议/总理事会对GATT与《入世议定书》关系做出统一解释,并单独将出口税承诺纳入减让表;2重视DSB既有的裁决思路,根据WTO规则修改相关出口管制法规;3加强资源开采的法律管控,提高资源税的征收标准;4确保对内外资源需求企业的管制一致,优化出口许可管理,努力从WTO法和国内法两个层面推动现行自然资源出口秩序的完善,使中国今后对自然资源的出口管制既能符合WTO规则又能达致确保本国经济可持续性发展之目的。